US5372831A - Treatment of coffee oil - Google Patents

Treatment of coffee oil Download PDF

Info

Publication number
US5372831A
US5372831A US08/025,626 US2562693A US5372831A US 5372831 A US5372831 A US 5372831A US 2562693 A US2562693 A US 2562693A US 5372831 A US5372831 A US 5372831A
Authority
US
United States
Prior art keywords
oil
filter
filtered
coffee
filtration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US08/025,626
Other languages
English (en)
Inventor
Peter Koch
Jean-Michel Parchet
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nestec SA
Original Assignee
Nestec SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nestec SA filed Critical Nestec SA
Assigned to NESTEC S.A. reassignment NESTEC S.A. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: KOCH, PETER, PARCHET, JEAN-MICHEL
Application granted granted Critical
Publication of US5372831A publication Critical patent/US5372831A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
    • A23F5/46—Coffee flavour; Coffee oil; Flavouring of coffee or coffee extract
    • A23F5/48—Isolation or recuperation of coffee flavour or coffee oil
    • A23F5/486—Isolation or recuperation of coffee flavour or coffee oil by distillation from beans that are ground or not ground, e.g. stripping; Recovering volatile gases, e.g. roaster or grinder gases
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
    • A23F5/46—Coffee flavour; Coffee oil; Flavouring of coffee or coffee extract
    • A23F5/48—Isolation or recuperation of coffee flavour or coffee oil

Definitions

  • This invention relates to a process for treating a coffee oil intended to be contacted with a frost charged with coffee aromas.
  • an oil generally a coffee oil
  • coffee aromas are enriched with coffee aromas and then sprayed onto the soluble coffee powder.
  • the main source used for the aromas are the aromas given off by the ground roasted coffee.
  • an inert gas such as carbon dioxide
  • This inert gas becomes charged with aromas, and a frost is formed by condensation of the carbon dioxide-entrained moisture and aromas.
  • This frost is then contacted with an oil which thus partly recovers the aromas present in the frost.
  • This may be done by directly contacting the oil with the frost consisting of carbon dioxide, water and aromas.
  • Another method of contacting is to sublimate the carbon dioxide and to contact the residual aqueous phase charged with aromas with the oil.
  • the oil obtained, which is enriched with aromas may then be re-incorporated in a soluble coffee powder.
  • the coffee oil may be an oil obtained by pressing roasted coffee which has not been extracted or, more often, an oil obtained from the grounds resulting from the extraction of ground roasted coffee with water.
  • the oil obtained from non-extracted roasted coffee produces by-products, such as the press cake, which are difficult to utilize.
  • the pressing of non-extracted roasted coffee involves losses of aromas which escape during pressing on are destroyed by the temperatures reached during pressing.
  • the problem addressed by the present invention was to provide a process for treating coffee oil before it is contacted with the frost charged with aromas which would enable a readily decantable emulsion of oil and water to be obtained.
  • the present invention provides a process for treating a coffee oil intended to be contacted either with a frost consisting of carbon dioxide, water and coffee aromas or with the residual aqueous phase charged with aromas obtained after sublimation of the carbon dioxide present in the frost, in which the coffee oil is filtered beforehand, the temperature of the oil being below 30° C. during the filtration step.
  • FIG. 1 diagrammatically illustrates an oil filtration unit for carrying out the process according to the invention.
  • the filtration unit for carrying out the process according to the invention may be formed by a feed reservoir 1 in which the oil to be treated is placed.
  • This reservoir is kept at a temperature set by a device which has not been shown, for example in the form of a coil immersed in the oil bath stirred by an agitator (not shown).
  • the temperature of the oil is preferably kept between 18° C. and 25° C. because, below 15° C., the oil becomes too viscous to be filtered.
  • the feed reservoir 1 is connected by a feed pipe 2, equipped with a valve 21, to one (or more) a filter assembly, or assemblies, which have a detachable outer envelope 4 provided with a vent 5, a cylindrical filtration surface 6 and an outlet pipe 7, for the filtered oil, connected to a filtered oil storage reservoir 9 which itself is connected to means 8 for establishing a partial vacuum.
  • each filter 3 consists of two concentric spaces separated by the filtration surface 6, the outer space 31, defined by the outer envelope 4 and the filtration surface 6, being connected to the feed reservoir 1, and the inner space 32 being connected to the means 8 for establishing a partial vacuum and to the storage reservoir 9.
  • the installation preferably comprises two filters 3 intended to operate in alternation.
  • the filters 3 are filled by gravity by opening the feed valve 21 and the vent 5 of the outer envelope 4 until the oil reaches the level of the vent 5, filling the outer space 31. After closure of the valve 21 and the vent 5, the inner space 32 which is situated on the other side of the filtration surface 6, is placed under a partial vacuum by the means 8. During filtration, the oil passes inwards through the filtration surface 6, flowing into the storage reservoir 9.
  • the filtration head of variable volume is preferably directed into the feed reservoir 1 until the oil obtained is clear.
  • the filtration head is understood to be the volume of oil which flows at the beginning of the filtration process.
  • a clear oil is an oil which has no turbidity when examined by transparency in a test tube placed in front of a light source.
  • filtration is preferably limited to a certain time dependent upon the installation used. At the end of this time, filtration is stopped and the unfiltered oil still present in the outer space 31 is directed to the feed reservoir 1.
  • the detachable outer envelope 4 may be removed, and the deposit formed on the filtration surface 6 may thus be scraped by suitable means. Thereafter, steam under pressure is injected, in the opposite direction to filtration, through the outlet 7 from a steam source 10 into the inner space 32, i.e., outwards. The deposit which is not recovered by scraping is rapidly liquefied and eliminated. The filter is then dried and cooled by the passage of air under pressure.
  • the total duration of this filter cleaning phase is an important parameter to be taken into account in the setting of the filtration time mentioned above. More particularly, to be able to operate continuously with two filters operating in alternation, the filtration time is preferably at least equal to the cleaning time. This is because, during the cleaning of one filter, the filtration process is continued in another filter.
  • the starting oil was the same and was filtered for 2 hours at 20° C. under a residual pressure of 100 mm Hg.
  • the pore size of the filtration surface only appears to be instrumental in determining the time required for the formation of a preliminary layer sufficient to enable the clear oil to be obtained. It only appears to determine the volume of the filtration head which has to be recycled to the feed reservoir. Since the pore size of the filtration surface is dependent in particular upon the oil to be treated, it may readily be determined by experimentation.
  • Example 2 An oil obtained by pressing from grounds filtered by the process described in Example 1 and an identical, but non-filtered oil were contacted with a frost charged with coffee aromas, each producing an emulsion containing 30% water.
  • the emulsion produced with the filtered oil showed a stable separation surface between the oil and the water by simple decantation, whereas the emulsion formed with a non-filtered oil could not be separated by decantation, the emulsion being stable.
  • test 1 was carried out using a filtration head of excessively low volume so that, on the one hand, the oil obtained did not have the required clarity and, on the other hand, the emulsion produced after contacting of this oil with a frost charged with aromas decanted poorly whereas, for tests 2, 3 and 4, decantation was entirely satisfactory.
  • a more stable emulsion is understood to be an emulsion which decants less quickly, if at all, or which, after decantation, produces an interface where emulsion residues remain.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Tea And Coffee (AREA)
  • Fats And Perfumes (AREA)
  • Lubricants (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Edible Oils And Fats (AREA)
US08/025,626 1992-03-16 1993-03-02 Treatment of coffee oil Expired - Lifetime US5372831A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP92104455A EP0561009B1 (de) 1992-03-16 1992-03-16 Verfahren zur Behandlung von Kaffee-Öl, bestimmt um mit einem Kaffeearoma enthaltenden Gefrierkondensat aufgenommen zu werden
EP92104455 1992-03-16

Publications (1)

Publication Number Publication Date
US5372831A true US5372831A (en) 1994-12-13

Family

ID=8209434

Family Applications (1)

Application Number Title Priority Date Filing Date
US08/025,626 Expired - Lifetime US5372831A (en) 1992-03-16 1993-03-02 Treatment of coffee oil

Country Status (14)

Country Link
US (1) US5372831A (de)
EP (1) EP0561009B1 (de)
JP (1) JP3022034B2 (de)
KR (1) KR0168881B1 (de)
AT (1) ATE139083T1 (de)
AU (1) AU659718B2 (de)
BR (1) BR9301174A (de)
CA (1) CA2091276A1 (de)
DE (1) DE69211528T2 (de)
DK (1) DK0561009T3 (de)
ES (1) ES2089267T3 (de)
GR (1) GR3021018T3 (de)
MA (1) MA22823A1 (de)
MX (1) MX9301378A (de)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5714094A (en) * 1994-07-23 1998-02-03 Nestec S.A. Antioxidant composition and process for the preparation thereof
US6699518B2 (en) 2001-01-23 2004-03-02 Kraft Foods Holdings, Inc. Method of preparing coffee aromatizing compositions

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3035921A (en) * 1959-05-06 1962-05-22 Robert W Carve Manufacture of soluble coffee
US3535118A (en) * 1964-12-31 1970-10-20 Kroger Co Method of making aromatized oil
US3903312A (en) * 1970-05-01 1975-09-02 Gen Foods Corp Process for producing aromatized freeze dried coffee
US4156031A (en) * 1975-07-07 1979-05-22 General Foods Corporation Stabilization of purified coffee oil
US4335149A (en) * 1980-06-02 1982-06-15 The Procter & Gamble Company Direct condensation of food volatiles onto a food substrate at cryogenic temperatures

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1206296A (en) * 1967-10-04 1970-09-23 Gen Foods Corp Production of soluble coffee
CA1083881A (en) * 1977-08-25 1980-08-19 General Foods, Lmited Separation and recovery of coffee aroma constituents from roasted coffee

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3035921A (en) * 1959-05-06 1962-05-22 Robert W Carve Manufacture of soluble coffee
US3535118A (en) * 1964-12-31 1970-10-20 Kroger Co Method of making aromatized oil
US3903312A (en) * 1970-05-01 1975-09-02 Gen Foods Corp Process for producing aromatized freeze dried coffee
US4156031A (en) * 1975-07-07 1979-05-22 General Foods Corporation Stabilization of purified coffee oil
US4335149A (en) * 1980-06-02 1982-06-15 The Procter & Gamble Company Direct condensation of food volatiles onto a food substrate at cryogenic temperatures

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
Sivetz, et al. Coffee Processing Technology, vol. 2, pp. 1 5, 21 30, and 175 182 (1963). *
Sivetz, et al. Coffee Processing Technology, vol. 2, pp. 1-5, 21-30, and 175-182 (1963).
Sivetz, et al., Coffee Technology, pp. 452 460, 568 571 (1979). *
Sivetz, et al., Coffee Technology, pp. 452-460, 568-571 (1979).

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5714094A (en) * 1994-07-23 1998-02-03 Nestec S.A. Antioxidant composition and process for the preparation thereof
US6699518B2 (en) 2001-01-23 2004-03-02 Kraft Foods Holdings, Inc. Method of preparing coffee aromatizing compositions

Also Published As

Publication number Publication date
KR930019119A (ko) 1993-10-18
JP3022034B2 (ja) 2000-03-15
EP0561009A1 (de) 1993-09-22
CA2091276A1 (en) 1993-09-17
GR3021018T3 (en) 1996-12-31
AU659718B2 (en) 1995-05-25
DK0561009T3 (da) 1996-09-09
MX9301378A (es) 1993-09-01
AU3405793A (en) 1993-09-23
EP0561009B1 (de) 1996-06-12
MA22823A1 (fr) 1993-10-01
ATE139083T1 (de) 1996-06-15
JPH06261687A (ja) 1994-09-20
DE69211528T2 (de) 1996-10-10
DE69211528D1 (de) 1996-07-18
BR9301174A (pt) 1993-11-30
ES2089267T3 (es) 1996-10-01
KR0168881B1 (ko) 1998-12-01

Similar Documents

Publication Publication Date Title
CA1333403C (en) Method of refining glyceride oils
US10406453B2 (en) Cannabinoid extraction process using brine
EP0094252B1 (de) Raffinierung von rohen Glyceridöl-Zusammensetzungen
JPS6017478B2 (ja) 植物油の処理法
US5372831A (en) Treatment of coffee oil
US5286886A (en) Method of refining glyceride oils
CS269985B2 (en) Method of perfluorpolyether oils cleaning
JPS60234548A (ja) 脱カフエイン紅茶の製法および製造装置
CA1240549A (en) Coffee oil treatment
JPH04293451A (ja) 可溶性インスタントコーヒーの製造法
JP5301214B2 (ja) コーヒー組成物の製造方法
CA1091504A (en) Decaffeination process
US2216905A (en) Treatment of distillery slop
US6656364B1 (en) Method for purifying contaminated liquids
JPH08283773A (ja) 化学合成添加物無添加サラダ油製造方法
US2141798A (en) Distillate treating process
CN113072969A (zh) 一种木醋液加工工艺
EP0636402A2 (de) Verfahren zur Vorbehandlung eines porösen Mediums
US4446162A (en) Decaffeination of a coffee extract
JPH06165640A (ja) 水出しコーヒーの製造方法及び装置
CA1188145A (en) Decaffeination of a coffee extract
KR20250043060A (ko) 들기름 또는 참기름의 제조 방법
CN121698433A (zh) 一种烟用爆珠滴制生产冷却液的回收工艺及回收设备
KR910005275B1 (ko) 고추의 농축액 제조방법 및 그 장치
EP0238451A2 (de) Verfahren zur Raffinierung von wachshaltenden Ölen zur Nahrungsverwendung

Legal Events

Date Code Title Description
AS Assignment

Owner name: NESTEC S.A., SWAZILAND

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:KOCH, PETER;PARCHET, JEAN-MICHEL;REEL/FRAME:006494/0812

Effective date: 19930215

STCF Information on status: patent grant

Free format text: PATENTED CASE

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

FPAY Fee payment

Year of fee payment: 12